2017
DOI: 10.1016/j.apcatb.2016.09.030
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Ethanolysis of Kraft lignin to platform chemicals on a MoC1-x/Cu-MgAlOz catalyst

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Cited by 85 publications
(59 citation statements)
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“…[b] Conversions take into account the 19.5 wt % of inorganic material (non‐depolymerizable) present in the lignin starting material. [c] The amount of catalyst added was 160 mg. [d] Data from Li and co‐workers …”
Section: Resultsmentioning
confidence: 99%
See 1 more Smart Citation
“…[b] Conversions take into account the 19.5 wt % of inorganic material (non‐depolymerizable) present in the lignin starting material. [c] The amount of catalyst added was 160 mg. [d] Data from Li and co‐workers …”
Section: Resultsmentioning
confidence: 99%
“…At 280 °C, Mo/Al 2 O 3 gave the highest yield of aromatics (330 mg g −1 lignin), however, α‐MoC 1− x /activated carbon (AC) gave the best overall yield of liquid products (classified as esters, aliphatic alcohols, and aromatics). To improve the process even further, Li and co‐workers reported the ethanolysis with an α‐MoC 1− x /Cu‐MgAlO z composite catalyst, which combines the virtues of both the catalysts previously reported by the Li and Hensen groups . Both the physical mixture of the components and the composite catalyst afforded higher overall yields of products than either MoC 1− x or Cu‐MgAlO z alone, in which the highest reported yield of aromatics is 575 mg g −1 lignin if the temperature was pushed to 330 °C.…”
Section: Introductionmentioning
confidence: 99%
“…Some processes that shown advantages in laboratory tests are not included primarily due to complexity of product mixture, large amounts of by‐products (e. g. char, coke and solve‐derived by‐products),, process instability (e. g. the yields of C0‐phenols are greatly affected by slight change of operation conditions),,, expensive operation medium (e. g. ionic liquid systems and B(C 6 F 5 ) 3 ) or lack of attractive data (e. g. methods based on photo‐ and electro‐ chemistry).…”
Section: The Promising Processes and Productsmentioning
confidence: 99%
“…As a hydrogen donor, alcohols used in lignin depolymerization can suppress the condensation of the phenolic intermediates. 10 In this paper, the catalytic activities of the ATP-supported catalysts were tested at 225 C in ethanol.…”
Section: Catalytic Activitymentioning
confidence: 99%
“…Chen et al 9 use mesoporous SBA-15 catalysts to depolymerize hydrolyzed lignin and eliminate char in ethanol and the results demonstrate that both catalyst and ethanol play important roles in suppressing the repolymerization reaction. Yan et al 10 have reported the depolymerization of kra lignin in supercritical ethanol on a MoC 1Àx /Cu-MgAlO z composite catalyst and a yield of aromatic compounds of 575 mg g À1 lignin is achieved at 330 C. Hidajat et al 11 report the base-catalyzed depolymerization of lignin in supercritical methanol and they nd that the most abundant monomers produced are methoxylated benzene and toluene species because of the unique O-alkylation ability of supercritical methanol. Kim et al 12 illustrate that lignin can be selectively degraded to alkylated phenols efficiently in supercritical t-BuOH as the M w of lignins decrease aer a supercritical t-BuOH treatment, which demonstrating the effectiveness of this method for lignin depolymerization.…”
mentioning
confidence: 99%